JPH0112760B2 - - Google Patents

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Publication number
JPH0112760B2
JPH0112760B2 JP57081505A JP8150582A JPH0112760B2 JP H0112760 B2 JPH0112760 B2 JP H0112760B2 JP 57081505 A JP57081505 A JP 57081505A JP 8150582 A JP8150582 A JP 8150582A JP H0112760 B2 JPH0112760 B2 JP H0112760B2
Authority
JP
Japan
Prior art keywords
interferon
solution
human interferon
human
carrier
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP57081505A
Other languages
Japanese (ja)
Other versions
JPS58201794A (en
Inventor
Kazuo Hosoi
Hitoshi Ozawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP57081505A priority Critical patent/JPS58201794A/en
Priority to CA000427891A priority patent/CA1213216A/en
Priority to US06/494,021 priority patent/US4541952A/en
Priority to DE8383104821T priority patent/DE3361838D1/en
Priority to SU833593070A priority patent/SU1523046A3/en
Priority to EP83104821A priority patent/EP0094672B1/en
Priority to UA3593070A priority patent/UA6303A1/en
Publication of JPS58201794A publication Critical patent/JPS58201794A/en
Publication of JPH0112760B2 publication Critical patent/JPH0112760B2/ja
Priority to LV930959A priority patent/LV5408A3/en
Priority to LTRP1024A priority patent/LT2589B/en
Priority to MD94-0031A priority patent/MD48C2/en
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K14/00Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/52Cytokines; Lymphokines; Interferons
    • C07K14/555Interferons [IFN]
    • C07K14/565IFN-beta
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00Chemistry: molecular biology and microbiology
    • Y10S435/811Interferon

Description

【発明の詳細な説明】 本発明はインターフエロンの濃縮精製法に関す
るものである。 インターフエロンは生きている細胞をウイルス
または特別の試剤等で刺激することによつて細胞
から産生される蛋白質であり、その化学構造は動
物種によつて異なり、また同じ動物種においても
複数のインターフエロン種が知られている。また
産生細胞種によつても多少異なる。 細胞または細胞外液から回収されるインターフ
エロンは、これで動物の組織または細胞を処理す
ると広範囲のウイルスに対する保護効果を生じさ
せる。インターフエロンは抗ウイルス活性として
ウイルス種に対する非特異性とインターフエロン
を産生した細胞と同一種の組織および細胞に対し
ては有効な抗ウイルス活性を与えるものの他種の
組織および細胞に対しては多くの場合無効であつ
たり、弱い抗ウイルス活性しか与えないという動
物種特異性が知られている。インターフエロンの
作用として抗ウイルス活性以外に抗腫疸性、細胞
増殖抑制作用、マクロフアージの機能促進その他
の多面的な作用が知られている。(「インターフエ
ロン研究の進歩」(蛋白質核酸酵素別冊第25号、
共立出版、1981年)、小林茂保著「増補版インタ
ーフエロン−基礎研究から臨床応用への展望」
(1978年・講談社サイエンテイフイク)等参照。) このためインターフエロンはウイルス性疾患例
えばB型肝炎、ヘルペス、インフルエンザ等の治
療薬または予防薬として、さらに脳腫瘍、骨肉
腫、白血病その他の抗ガン剤としても期待されて
いる。 ここでヒトに投与されるべきインターフエロン
は先に述べたインターフエロンの種特異性のため
ヒトインターフエロンでなければならずこれは天
然においてはヒト細胞によつて産生される。 現在、ヒトインターフエロンはヒトインターフ
エロンα、βおよびγの三種に分類されている。 ヒトインターフエロンαはヒト白血球細胞によ
つて産生されるインターフエロンに代表され、ヒ
トインターフエロンβはヒト二倍体線維芽細胞に
よつて産生されるインターフエロン(ヒトフイブ
ロブラストインターフエロン)に代表される。ま
た、ヒトインターフエロンγは、Tリンパ球細胞
によつて産生されるインターフエロンである。 本発明は、これらヒトインターフエロンの濃縮
精製法に関するものであり、特にヒトインターフ
エロンβの濃縮精製に最適な方法を提供するもの
である。 ヒトインターフエロンβは、通常、ガラスもし
くはプラスチツク等の表面またはDEAE化デキス
トランのマイクロキヤリア−表面上等で培養され
たヒトインターフエロンβ産生細胞(以後単に細
胞と略すことがある)を例えばPolyI:Cのよう
な合成二本鎖RNAによる誘発処理と続いて行な
う超誘発処理(例えばシクロヘキシミドとアクチ
ノマイシンDの組合せによる代謝阻害法または紫
外線照射法等)に付した後、細胞を培養液中に20
〜48時間培養することにより、この培養液中に産
生され、ヒトインターフエロンβを含有する産生
液として取得される。 この場合、培養液としては、例えばイーグル
MEM培養液が用いられ、必要に応じ血清および
種々の添加物が加えられる。もちろんこれ以外の
培養液が用いられる場合もありうる。 このようにして得られるヒトインターフエロン
を含有している産生液中のヒトインターフエロン
は一般的に低濃度〔数千〜数万単位(生物学的検
定法により、NIH供与ヒトインターフエロンリ
フアランススタンダードで換算した力価すなわち
国際単位を示す)/ml〕であり、この産生液には
ヒトインターフエロンの他に細胞由来、培養由来
または添加物由来の多くの夾雑物を含んでいるの
で医療に用いるにはヒトインターフエロンを濃縮
精製することが要求されている。 純品としてのヒトインターフエロンの生物学的
活性は蛋白質1mg当り0.4〜1×109単位と言われ
ている。 従来から、ヒトインターフエロンの濃縮精製法
について多くの方法が報告されている。例えば硫
酸アンモニウムを用いる沈澱法、中空繊維限外
過膜を使用する膜濃縮法、CM−セフアデツクス
を用いるイオン交換法、セフアデツクスやポリア
クリルアミドゲル等を用いる分子ふるい法等が知
られている。 ヒトインターフエロンβのもつ疎水性を利用し
て疎水性担体、例えばコンカナバリンA、オクチ
ル基、トリプトフイル基、フエニル基等を導入し
たアガロースゲルを用いる疎水性クロマトグラフ
イーによるヒトインターフエロンの濃縮精製法も
知られている。〔W.A.Carterら、Biochemistry
15、704(1976);J.Biol.Chem.251、5381(1976);
ibid.251、7260(1976)〕。 近年、下式の化学構造を有する色素を結合させ
た担体を用いるインターフエロンの精製が知られ
ている。この色素はCIBA−GEIGY社から“シ
バクロンブルーF3GA”または“シバクロンブル
ー3GA”なる商品名で売られている青色色素で
あり、一般名はCIリアクテイブブルー2である。 上記色素を結合させた担体を用いるヒトおよび
動物のインターフエロンの精製および示性化が
Jankowskiらによつて「Biochemistry」第15巻
第5182〜5187頁(1976)に、またBollinらによつ
て「Preparative Biochemistry」第8巻第259〜
292頁(1978)に、またEricksonらによつて
「Archives of Virology」第63巻、第253〜261頁
(1980)に示されている。 E.ナイトらは特開昭50−61997において粗ヒト
インターフエロンβ溶液を、架橋アガロースゲル
に上記色素を結合させた“ブルーセフアロース”
(フアルマシア社製)にかけ比活性4×108単位/
mg・蛋白質で純度95%以上の精製ヒトインターフ
エロンβを収率50%で得たと主張している。 しかし、ここで精製されたヒトインターフエロ
ンβを注射用商品とするには含有されるエチレン
グリコールおよび高濃度の塩化ナトリウムを除去
するいわゆる脱塩工程が必要である。脱塩するた
めには、例えば“セフアデツクスG−25”を用い
るゲル過法や透析などの手段があるが、エチレ
ングリコールが高粘性を有するため、その十分な
除去は難かしい。また単に“ブルーセフアロー
ズ”での精製では、発熱性物質の除去が必ずしも
十分でなく、注射用に供するには問題がある。 また“ブルーセフアローズ”は、インターフエ
ロンの産生に使用したアクチノマイシンDに対し
て親和性があり、インターフエロン回収区分には
アクチノマイシンDが混入されやすい。アクチノ
マイシンDは抗ガン剤として用いられているもの
の、一方強い突然変異原であり、その混入が認め
られることは極めて大きな問題点となる。 さらに本発明と関連のある亜鉛キレート担体カ
ラムクロマトグラフイーを用いるものとしてV.
G.Edyらの方法が知られている〔J.Biol.Chem.
252、5934(1978)〕。Edyらは、亜鉛キレート担体
カラム容量の約14倍の粗F−IF溶液(2万IU/
ml、蛋白質含量0.4mg/ml)を中性条件下カラム
に通夜してF−IFをカラムに吸着させた後、酸
性溶出液を用いて32倍精製されたF−IFの溶液
を得ている。また溶出液PHグラデイエント法を用
いて3100倍精製された蛋白質1mg当り108
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for concentrating and purifying interferon. Interferon is a protein produced by living cells by stimulating them with a virus or special agent, and its chemical structure differs depending on the animal species, and even in the same animal species, multiple interferons are produced. Elon species are known. It also varies somewhat depending on the type of producing cell. Interferons recovered from cells or extracellular fluids produce protective effects against a wide range of viruses when treated with animal tissues or cells. Interferon has antiviral activity that is nonspecific to virus species and has effective antiviral activity against tissues and cells of the same species as the cells that produced interferon, but has a high antiviral activity against tissues and cells of other species. It is known to be species-specific in that it is ineffective or only provides weak antiviral activity in some cases. In addition to its antiviral activity, interferon is known to have antitumor properties, cell proliferation inhibitory effects, promotion of macrophage function, and other multifaceted effects. (“Advances in Interferon Research” (Protein Nucleic Acid Enzyme Special Issue No. 25,
Kyoritsu Shuppan, 1981), Shigeyasu Kobayashi, "Expanded edition of Interferon - Prospects from basic research to clinical application"
(1978, Kodansha Scientific), etc. Therefore, interferon is expected to be used as a therapeutic or preventive drug for viral diseases such as hepatitis B, herpes, and influenza, and as an anticancer agent for brain tumors, osteosarcoma, leukemia, and other diseases. Here, the interferon to be administered to humans must be human interferon because of the species specificity of interferon mentioned above, which is naturally produced by human cells. Currently, human interferon is classified into three types: human interferon α, β, and γ. Human interferon α is represented by interferon produced by human white blood cells, and human interferon β is represented by interferon (human fibroblast interferon) produced by human diploid fibroblasts. be done. Human interferon gamma is also an interferon produced by T lymphocytes. The present invention relates to a method for concentrating and purifying human interferon, and particularly provides an optimal method for concentrating and purifying human interferon β. Human interferon β is usually produced by human interferon β producing cells (hereinafter sometimes simply referred to as cells) cultured on a surface such as glass or plastic or on a microcarrier surface of DEAE-modified dextran. After induction treatment with synthetic double-stranded RNA such as
By culturing for ~48 hours, human interferon β is produced in this culture solution and obtained as a production solution containing human interferon β. In this case, as the culture solution, for example, Eagle
MEM culture medium is used, and serum and various additives are added as necessary. Of course, other culture solutions may be used. The human interferon in the production solution containing human interferon obtained in this way is generally at a low concentration [several thousand to tens of thousands of units (by biological assay, it is determined by the NIH-provided human interferon rebalance standard). This product is used for medical purposes because it contains many impurities derived from cells, culture, or additives in addition to human interferon. It is required to concentrate and purify human interferon. The biological activity of pure human interferon is said to be 0.4 to 1×10 9 units per mg of protein. Many methods have been reported for enriching and purifying human interferon. For example, a precipitation method using ammonium sulfate, a membrane concentration method using a hollow fiber ultrafiltration membrane, an ion exchange method using CM-Sephadex, a molecular sieving method using Sephadex, polyacrylamide gel, etc. are known. Utilizing the hydrophobicity of human interferon β, there is also a method for concentrating and purifying human interferon by hydrophobic chromatography using a hydrophobic carrier such as concanavalin A, an octyl group, a tryptopyl group, a phenyl group, etc., introduced into agarose gel. Are known. [WA Carter et al., Biochemistry
15, 704 (1976); J.Biol.Chem. 251 , 5381 (1976);
ibid. 251 , 7260 (1976)]. In recent years, it has been known to purify interferon using a carrier bound with a dye having the chemical structure shown below. This pigment is a blue pigment sold by CIBA-GEIGY under the trade name "Cibacron Blue F3GA" or "Cibacron Blue 3GA", and its general name is CI Reactive Blue 2. Purification and characterization of human and animal interferon using carriers bound with the above dyes
Jankowski et al., Biochemistry, Vol. 15, pp. 5182-5187 (1976), and Bollin et al., Preparative Biochemistry, Vol.
292 (1978) and by Erickson et al. in Archives of Virology, Vol. 63, pp. 253-261 (1980). In JP-A-50-61997, E. Knight et al. used a crude human interferon β solution to bind the above dye to a cross-linked agarose gel to produce "Bluecephalose".
(manufactured by Pharmacia) with specific activity of 4 x 10 8 units/
The company claims to have obtained purified human interferon-β with a purity of 95% or higher in mg/protein at a yield of 50%. However, in order to use the purified human interferon β as an injectable product, a so-called desalting process is required to remove the ethylene glycol and high concentration of sodium chloride contained therein. For desalting, there are methods such as gel filtration using "Sephadex G-25" or dialysis, but since ethylene glycol has high viscosity, it is difficult to remove it sufficiently. Furthermore, simply purifying with "Blue Cepharose" does not necessarily remove pyrogens sufficiently, which poses a problem for use in injections. Furthermore, "Bluecephalus" has an affinity for actinomycin D used in the production of interferon, and actinomycin D is likely to be mixed into the interferon recovery section. Although actinomycin D is used as an anticancer drug, it is also a strong mutagen, and its contamination is an extremely serious problem. Furthermore, V.
The method of G. Edy et al. is known [J. Biol. Chem.
252, 5934 (1978)]. Edy et al. reported that the crude F-IF solution (20,000 IU/
ml, protein content 0.4 mg/ml) was left on a column under neutral conditions overnight to adsorb F-IF onto the column, and then an acidic eluate was used to obtain a 32-fold purified solution of F-IF. . In addition, 10 8 per mg of protein was purified 3100 times using the eluate PH gradient method.

Claims (1)

【特許請求の範囲】[Claims] 1 粗ヒトインターフエロンβ溶液を、CIリア
クテイブブルー2と架橋アガロースゲルがエーテ
ル結合で結ばれている不溶性ブルー担体と接触さ
せ、該インターフエロンを該ブルー担体に吸着さ
せた後、溶出液を用いて該インターフエロンを溶
液として回収し、ついで該インターフエロン回収
液をコバルト、ニツケル及び亜鉛からなる群から
選ばれた少なくとも一つの金属をキレート化させ
たキレート基結合担体に接触させ、該インターフ
エロンを該キレート基結合担体に吸着させた後、
溶出液を用いて該インターフエロンを溶液として
回収することを特徴とするヒトインターフエロン
βの濃縮精製法。
1. Contact the crude human interferon β solution with an insoluble blue carrier in which CI Reactive Blue 2 and crosslinked agarose gel are linked by ether bonds, and after adsorbing the interferon to the blue carrier, use the eluate. The interferon is recovered as a solution, and then the interferon recovery liquid is brought into contact with a chelate group-bonded carrier chelated with at least one metal selected from the group consisting of cobalt, nickel, and zinc, and the interferon is recovered as a solution. After adsorption to the chelate group-bonded carrier,
A method for concentrating and purifying human interferon β, which comprises recovering the interferon as a solution using an eluate.
JP57081505A 1982-05-17 1982-05-17 Purification of human interferon through concentration Granted JPS58201794A (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
JP57081505A JPS58201794A (en) 1982-05-17 1982-05-17 Purification of human interferon through concentration
CA000427891A CA1213216A (en) 1982-05-17 1983-05-11 Purification method of human interferon
US06/494,021 US4541952A (en) 1982-05-17 1983-05-12 Purification method of human interferon
EP83104821A EP0094672B1 (en) 1982-05-17 1983-05-16 Purification method of human interferon
SU833593070A SU1523046A3 (en) 1982-05-17 1983-05-16 Method of purifying human beta-interferon
DE8383104821T DE3361838D1 (en) 1982-05-17 1983-05-16 Purification method of human interferon
UA3593070A UA6303A1 (en) 1982-05-17 1983-05-16 Method for purifying human interferon beta
LV930959A LV5408A3 (en) 1982-05-17 1993-06-30 Decrease in human beta-interferon depletion
LTRP1024A LT2589B (en) 1982-05-17 1993-09-21 THE HUMAN ALPHA -INTERFERENCE CHOICE
MD94-0031A MD48C2 (en) 1982-05-17 1993-11-12 Method for human b-interferon purification

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57081505A JPS58201794A (en) 1982-05-17 1982-05-17 Purification of human interferon through concentration

Publications (2)

Publication Number Publication Date
JPS58201794A JPS58201794A (en) 1983-11-24
JPH0112760B2 true JPH0112760B2 (en) 1989-03-02

Family

ID=13748211

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57081505A Granted JPS58201794A (en) 1982-05-17 1982-05-17 Purification of human interferon through concentration

Country Status (7)

Country Link
US (1) US4541952A (en)
EP (1) EP0094672B1 (en)
JP (1) JPS58201794A (en)
CA (1) CA1213216A (en)
DE (1) DE3361838D1 (en)
SU (1) SU1523046A3 (en)
UA (1) UA6303A1 (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES8302096A1 (en) 1980-04-03 1982-12-16 Biogen Nv DNA sequences, recombinant DNA molecules and processes for producing human fibroblast interferon.
US4723000A (en) * 1983-07-05 1988-02-02 Biospectrum, Inc. Human interferon gamma and interleukin-2
US4530787A (en) * 1984-03-28 1985-07-23 Cetus Corporation Controlled oxidation of microbially produced cysteine-containing proteins
JPS6169799A (en) * 1984-09-14 1986-04-10 Kyowa Hakko Kogyo Co Ltd Purification of interferon
ATE52425T1 (en) * 1985-02-04 1990-05-15 Hoffmann La Roche ADSORBENT FOR PURIFICATION OF PROTEINS.
US4960702A (en) * 1985-09-06 1990-10-02 Codon Methods for recovery of tissue plasminogen activator
US4732683A (en) * 1986-12-02 1988-03-22 Biospectrum, Inc. Purification method for alpha interferon
US4961969A (en) * 1987-05-11 1990-10-09 Cetus Corporation Process for recovering microbially produced interferon-β
US4808314A (en) * 1987-09-18 1989-02-28 Scripps Clinic And Research Foundation Method for reducing bacterial endotoxin contamination in solutions of macromolecules
US5597485A (en) * 1988-05-13 1997-01-28 Vilmax S.A. Process for separating proteins
US5034133A (en) * 1990-07-26 1991-07-23 Schering-Corporation Purification of human interleukin-4 from a CHO-cell line culture medium
US6479300B1 (en) * 1999-03-15 2002-11-12 Millipore Corporation Metal loaded ligand bound membranes for metal ion affinity chromatography
US7354721B2 (en) * 2000-09-22 2008-04-08 Clontech Laboratories, Inc. Highly sensitive proteomic analysis methods, and kits and systems for practicing the same
WO2002074806A2 (en) 2001-02-27 2002-09-26 Maxygen Aps New interferon beta-like molecules
US7176278B2 (en) 2001-08-30 2007-02-13 Biorexis Technology, Inc. Modified transferrin fusion proteins
KR100524871B1 (en) * 2003-12-04 2005-10-31 씨제이 주식회사 Processes for the purification of interferon beta
KR100524872B1 (en) * 2003-12-04 2005-11-01 씨제이 주식회사 Processes for the purification of interferon beta
DE102009032179A1 (en) 2009-07-07 2011-01-13 Biogenerix Ag Process for purifying interferon beta

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE27262C (en) * H. HEWITT in Birmingham Steel spring with ball point
DE11435C (en) * M. MERZBACH in Berlin C, Seydelstrafse 9 Locks for suitcases, chats, books, bag hangers and so on by means of a letter lock
JPS5564799A (en) * 1978-11-07 1980-05-15 Toray Ind Inc Multi-stage concentration and purification of interferon originated from human fibroblast
FI77877C (en) * 1979-04-20 1989-05-10 Technobiotic Ltd Process for the preparation and purification of human Le-shaped interferon protein.
US4289689A (en) * 1980-03-14 1981-09-15 Hoffmann-La Roche Inc. Preparation of homogeneous human fibroblast interferon
US4278661A (en) * 1979-10-12 1981-07-14 E. I. Du Pont De Nemours And Company Purification of interferon
NL7907791A (en) * 1979-10-23 1981-04-27 Stichting Rega V Z W METHOD FOR PURIFYING INTERFERON.

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
ARCH.VIROL.=1981 *
J.BIOL.CHEM.=1981 *
J.GEN.VIROL.=1980 *
SCAND.J.IMMUNOL.=1980 *

Also Published As

Publication number Publication date
EP0094672A1 (en) 1983-11-23
UA6303A1 (en) 1994-12-29
EP0094672B1 (en) 1986-01-15
US4541952A (en) 1985-09-17
JPS58201794A (en) 1983-11-24
SU1523046A3 (en) 1989-11-15
DE3361838D1 (en) 1986-02-27
CA1213216A (en) 1986-10-28

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